A multi-stage vacuum adiabatic flash continuous crystallization method and equipment
A vacuum adiabatic and flash evaporation technology, applied in the field of multi-stage vacuum adiabatic flash continuous crystallization process, continuous crystallization equipment, multi-stage vacuum adiabatic flash continuous crystallization method and equipment, can solve the impact of continuous operation of the device and slurry mixing Variation, crystal particle size and other problems, to achieve the effect of improving production efficiency, reducing the number of equipment, and maintaining stable particle size
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Embodiment 1
[0046] Such as figure 1 Shown, a continuous vacuum adiabatic flash evaporation continuous crystallizer. There is a thermal insulation layer 2 outside the crystallizer. The diameters of the upper and lower straight cylinders of the crystallizer are different. The diameter of the upper part is larger than that of the lower part. The diameter of the upper straight cylinder is 3.5 meters. The height of the segment is 2 meters. The hot material enters the inside of the guide tube 6 from the feed port 3, and is stirred by a double-layer large-diameter stirring paddle 7. The height of the guide tube is 1.7 meters, the diameter of the guide tube is 1.83 meters, and the diameter of the stirring paddle is It is 1.8 meters. The mixing in the crystallizer is uniform, and there is a spray pipe 1 on the upper part of the crystallizer for spraying the inner wall of the crystallizer to remove the knot wall at the evaporation surface. The evaporated water in the crystallizer is condensed by...
Embodiment 2
[0048] Such as figure 2 Shown is a vacuum adiabatic flash evaporation continuous crystallization process; two crystallizers are connected in series. The top of the crystallizer is connected with a condenser and a water ring vacuum pump; the lower part of the crystallizer is equipped with a turbidimeter. The material inlet of each level of crystallizer is located at the bottom of the guide tube, which is higher than the stirring paddle of the lower layer; the material outlet is located at the bottom of the crystallizer; the discharge pipe of the last stage of crystallizer is connected to the centrifuge. The concentration in the storage tank 10 is 17%, and the sodium hydrogen phosphate mother liquor with a temperature of 80 degrees is entered into the first-stage crystallizer 12 by the centrifugal pump 11 according to the flow rate of 7m3 / h, and the first-stage crystallizer 12 is controlled by controlling the power of the water ring vacuum pump 15. The degree of vacuum in the ...
Embodiment 3
[0050] Such as image 3 Shown is a vacuum adiabatic flash evaporation continuous crystallization process; four crystallizers are connected in series. The top of the crystallizer is connected with a condenser and a water ring vacuum pump; the lower part of the crystallizer is equipped with a turbidimeter. The material inlet of each level of crystallizer is located at the bottom of the guide tube, which is higher than the stirring paddle of the lower layer; the material outlet is located at the bottom of the crystallizer; the discharge pipe of the last stage of crystallizer is connected to the centrifuge. The concentration in the storage tank 10 is 23%, and the sodium hydrogen phosphate mother liquor with a temperature of 90 degrees is entered into the first-stage crystallizer 12 by the centrifugal pump 11 according to the flow rate of 7m3 / h, and is controlled by controlling the power of the water ring vacuum pump 15 The degree of vacuum in the first-stage crystallizer makes th...
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